Oxidation-resistant composite reverse osmosis membrane
a reverse osmosis membrane and composite technology, applied in the field of reverse osmosis membranes, can solve the problems of reducing the water flux of the membrane, reducing the salt rejection of the membrane, and contaminating the polyamide ro membrane, so as to improve the performance of the reverse osmosis membrane, improve the resistance to oxidation and organic fouling, and prolong the li
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examples 1-2
[0072]Composite RO membranes as prepared in Comparative Example 1 were immersed in a 1% aqueous solution of potassium persulfate maintained at pH 8 by a potassium phosphate buffer for different times as shown in the following Table 1, and then dried in an oven at a temperature of 140° C. for 5 minutes to give composite RO membranes of the invention. The performances of the RO membranes were determined as described in the Comparative Example 1, and the results were shown in Table 1.
TABLE 1Performances of RO MembranesComparativeItemsExample 1Example 1Example 2Time for treatment with—1030potassium persulfate (min)Initial salt rejection (%)99.399.399.2Initial water flux (GFD)24.822.423.3After treatment with NaClOSalt rejection (%)5.886.998.8Water flux (GFD)56243.228.7
[0073]It can be found from the data as shown in Table 1 that the oxidation resistance of the RO membranes was significantly improved by the treatment with potassium persulfate.
examples 3-8
[0074]The porous support was immersed in a 2.5% solution of m-phenylenediamine (MPDA) containing 0.1 wt % of sodium dodecylbenzene sulfonate (SDBS) for about 1 min. The support was then drained and nip rolled to remove the excess aqueous solution. After that, the treated support was contacted with a 0.1% (wt / v %) solution of acid chloride in ethylhexane as shown in the following Table 2 for 50 seconds, and then dried in an oven at a temperature of 40° C. for 10 minutes to give a polyamide reverse osmosis membrane. The performances of the membrane were determined as described in Comparative Example 1, and the results were shown in Table 2.
TABLE 2Performances of RO Membranes as Prepared in Examples 3-8ItemsEx. 3Ex. 4Ex. 5Ex. 6Ex. 7Ex. 8Total concentration of acid0.10.10.10.10.10.1chlorideRelative concentration of08070504030TMC in the acid chloride (%)Relative concentration of 5-1002030506070iodo-isophthaloyl chloride (%)Initial salt rejection (%)98.999.199.399.399.299.1Initial water f...
example 9
[0076]An RO membrane was prepared according to the process as described in Example 6, except that the 5-iodo-isophthaloyl chloride was replaced by 2-iodo-terephthaloyl chloride. The performances of the membrane were determined as described in Comparative Example 1, and the results were shown in the following Table 3.
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